Regeneration gas aircooler thermal expansion.
Regeneration gas aircooler thermal expansion.
(OP)
I´m designing the regeneration gas aircooler of an NGL plant.
API 661 ask for methods of restraint relief for multipass bundles with temp. difference larger than 200°F, which is the case of this equipment.
I have tried multipass bundles (4 to 6 passes) with different tube pass configurations as side-side, crossed, a side-side/crossed mix, but in every case the first pass delta T is aprox 285°F. The second pass delta T is 100°F.
Our mechanical engineer said differential thermal expansion will damage the bundle, specially at header/tube union and a single pass cooler should be used.
On the other hand I had checked similar equipment of recognized companies (Smithco) and found even larger temperatures differences. (Gas is cooled from 550°F to 120°F in a 2-pass split box header bundle with 360°F & 70°F delta T for each pass).
I´m reluctant to design a single pass cooler as the heat transfer coeff inside the tubes will be very low, even lower than air, thus generating a very large cooler.
If someone has some experience on this matter it will be helpful.
Thank.
API 661 ask for methods of restraint relief for multipass bundles with temp. difference larger than 200°F, which is the case of this equipment.
I have tried multipass bundles (4 to 6 passes) with different tube pass configurations as side-side, crossed, a side-side/crossed mix, but in every case the first pass delta T is aprox 285°F. The second pass delta T is 100°F.
Our mechanical engineer said differential thermal expansion will damage the bundle, specially at header/tube union and a single pass cooler should be used.
On the other hand I had checked similar equipment of recognized companies (Smithco) and found even larger temperatures differences. (Gas is cooled from 550°F to 120°F in a 2-pass split box header bundle with 360°F & 70°F delta T for each pass).
I´m reluctant to design a single pass cooler as the heat transfer coeff inside the tubes will be very low, even lower than air, thus generating a very large cooler.
If someone has some experience on this matter it will be helpful.
Thank.





RE: Regeneration gas aircooler thermal expansion.
You already know that you need a split header because of the large temperature difference through the cooler. The question is, what is the best way to do it. My suggestion is to use either a 4-row/2-pass arrangement or possibly a 6-row/3-pass one. In the second case, I would suggest that the front header should be split between the first and second passes, since the largest temperature drop will likely occur in the first pass.
Regards,
Speco (www.stoneprocess.com)
RE: Regeneration gas aircooler thermal expansion.
A process engineer should specify all the possible operating cases for this aerial cooler including turndown, and low ambient temperature cases.
An experienced thermal designer should then investigate which operating case is the governing one on the basis of calculated mean metal temperatures of tubes in separate rows/passes.
You might need more than one split.
Regards,
S.
RE: Regeneration gas aircooler thermal expansion.
Speco
RE: Regeneration gas aircooler thermal expansion.
I´m aware that multiple split headers may be required.
Regarding other operating cases, I´m checking low air temp condition, but this is a warm climate location and freezing will not be and issue (but hidrates could form).
RE: Regeneration gas aircooler thermal expansion.
Cheers,
S.
RE: Regeneration gas aircooler thermal expansion.